JPH053376B2 - - Google Patents

Info

Publication number
JPH053376B2
JPH053376B2 JP7801585A JP7801585A JPH053376B2 JP H053376 B2 JPH053376 B2 JP H053376B2 JP 7801585 A JP7801585 A JP 7801585A JP 7801585 A JP7801585 A JP 7801585A JP H053376 B2 JPH053376 B2 JP H053376B2
Authority
JP
Japan
Prior art keywords
layer
resin
intermediate layer
multilayer
parison
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP7801585A
Other languages
Japanese (ja)
Other versions
JPS61235126A (en
Inventor
Yoshinori Nakamura
Hiroyuki Orimoto
Koichi Sato
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nissei ASB Machine Co Ltd
Original Assignee
Nissei ASB Machine Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=13649965&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=JPH053376(B2) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Priority to JP60078015A priority Critical patent/JPS61235126A/en
Application filed by Nissei ASB Machine Co Ltd filed Critical Nissei ASB Machine Co Ltd
Priority to US06/849,556 priority patent/US4743479A/en
Priority to CA000506204A priority patent/CA1271435A/en
Priority to AU55911/86A priority patent/AU588581B2/en
Priority to KR1019860002713A priority patent/KR940005636B1/en
Priority to DE86400768T priority patent/DE3688686T2/en
Priority to EP86400768A priority patent/EP0199633B1/en
Priority to NZ215789A priority patent/NZ215789A/en
Priority to ES553938A priority patent/ES8704382A1/en
Priority to CN86102410A priority patent/CN1006773B/en
Priority to BR8601821A priority patent/BR8601821A/en
Publication of JPS61235126A publication Critical patent/JPS61235126A/en
Priority to US06/941,022 priority patent/US4774047A/en
Publication of JPH053376B2 publication Critical patent/JPH053376B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C49/00Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
    • B29C49/22Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor using multilayered preforms or parisons
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/16Making multilayered or multicoloured articles
    • B29C45/164The moulding materials being injected simultaneously
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/16Making multilayered or multicoloured articles
    • B29C45/1642Making multilayered or multicoloured articles having a "sandwich" structure
    • B29C45/1646Injecting parison-like articles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/16Making multilayered or multicoloured articles
    • B29C45/1642Making multilayered or multicoloured articles having a "sandwich" structure
    • B29C45/1646Injecting parison-like articles
    • B29C2045/1648Injecting parison-like articles the parison core layer being a barrier material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/16Making multilayered or multicoloured articles
    • B29C45/1642Making multilayered or multicoloured articles having a "sandwich" structure
    • B29C2045/1656Injecting the skin material through the central passage of the multiway nozzle
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2949/00Indexing scheme relating to blow-moulding
    • B29C2949/30Preforms or parisons made of several components
    • B29C2949/3008Preforms or parisons made of several components at neck portion
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2949/00Indexing scheme relating to blow-moulding
    • B29C2949/30Preforms or parisons made of several components
    • B29C2949/3008Preforms or parisons made of several components at neck portion
    • B29C2949/3009Preforms or parisons made of several components at neck portion partially
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2949/00Indexing scheme relating to blow-moulding
    • B29C2949/30Preforms or parisons made of several components
    • B29C2949/3012Preforms or parisons made of several components at flange portion
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2949/00Indexing scheme relating to blow-moulding
    • B29C2949/30Preforms or parisons made of several components
    • B29C2949/3016Preforms or parisons made of several components at body portion
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2949/00Indexing scheme relating to blow-moulding
    • B29C2949/30Preforms or parisons made of several components
    • B29C2949/302Preforms or parisons made of several components at bottom portion
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2949/00Indexing scheme relating to blow-moulding
    • B29C2949/30Preforms or parisons made of several components
    • B29C2949/3024Preforms or parisons made of several components characterised by the number of components or by the manufacturing technique
    • B29C2949/3026Preforms or parisons made of several components characterised by the number of components or by the manufacturing technique having two or more components
    • B29C2949/3028Preforms or parisons made of several components characterised by the number of components or by the manufacturing technique having two or more components having three or more components
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2949/00Indexing scheme relating to blow-moulding
    • B29C2949/30Preforms or parisons made of several components
    • B29C2949/3032Preforms or parisons made of several components having components being injected
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2949/00Indexing scheme relating to blow-moulding
    • B29C2949/30Preforms or parisons made of several components
    • B29C2949/3032Preforms or parisons made of several components having components being injected
    • B29C2949/3034Preforms or parisons made of several components having components being injected having two or more components being injected
    • B29C2949/3036Preforms or parisons made of several components having components being injected having two or more components being injected having three or more components being injected
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2067/00Use of polyesters or derivatives thereof, as moulding material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/25Solid
    • B29K2105/253Preform
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/13Hollow or container type article [e.g., tube, vase, etc.]
    • Y10T428/1352Polymer or resin containing [i.e., natural or synthetic]
    • Y10T428/1379Contains vapor or gas barrier, polymer derived from vinyl chloride or vinylidene chloride, or polymer containing a vinyl alcohol unit
    • Y10T428/1383Vapor or gas barrier, polymer derived from vinyl chloride or vinylidene chloride, or polymer containing a vinyl alcohol unit is sandwiched between layers [continuous layer]
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/24Structurally defined web or sheet [e.g., overall dimension, etc.]
    • Y10T428/24942Structurally defined web or sheet [e.g., overall dimension, etc.] including components having same physical characteristic in differing degree
    • Y10T428/2495Thickness [relative or absolute]

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
  • Containers Having Bodies Formed In One Piece (AREA)
  • Laminated Bodies (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

(産業上の利用分野) この発明は中間層を有する合成樹脂製の多層容
器の製造方法に関するものである。 (従来の技術) 吹込または延伸吹込成形された合成樹脂の包装
用容器は、軽量で落下強度をも有するが、ガラス
に比べてガスバリヤー性が劣り酸素、炭酸ガス等
の透過を嫌う内容物の容器として使用する場合に
は、更に改良が必要とされていた。 そこで容器本体を形成する樹脂の内に、その樹
脂の欠点を補う他の樹脂を中間層として設けた少
なくとも3層の多層容器が開発されている。また
中間層としてはガスバリヤー性に優れたエチレ
ン・ビニルアルコール共重合体、ポリアミドなど
の樹脂が用いられている。 この多層構造の容器は、押出または射出成形さ
れた多層パリソンを、単層構造の場合と同様に、
吹込成形または延伸吹込成形して作ることがで
き、そこに形成された中間層は、容器本体を形成
している樹脂の真中か或は内側に位置している。
この中間層が真中に位置した容器本体では、中間
層によつて区画形成された内層と外層の2つの層
の肉厚に差は生じないが、中間層が内側に片寄つ
て位置した場合には、内外層の肉厚に差が生じ、
内層は外層に比べて著しく薄肉となる。 多層容器における各層の肉厚分布は、押出また
は射出成形された多層有底パリソンの肉厚分布に
よつて決定され、パリソンが有する肉厚の割合
が、そのまま容器の肉厚の割合となる。 多層有底パリソンの成形は、特公昭59−29416
号公報に記載されているように、ノズル口と連通
した外側流路と、その外側流路の先端部内にて開
口した内側流路とを備えた2重ノズルを用いて行
つており、パリソン形成樹脂は外側流路から、ま
た中間層形成樹脂は内側流路からそれぞれキヤビ
テイ内へ注入している。また2つの樹脂の注入量
によつて、中間層の肉厚を変化させることはでき
るけれども、中間層は常に内側に片寄つて生じ、
その結果、内層が薄肉に形成される。 (発明が解決しようとする問題点) エチレン・ビニルアルコール共重合体
(EVOH)、ポリアミド(PA)などの樹脂は、吸
湿量の増加に伴つて酸素、炭酸ガスなどの透過量
も増大する。一方炭酸飲料のびんとして用いられ
ている二軸延伸ポリエステルの樹脂は、上記樹脂
よりも透湿度が低いが、樹脂全般に云えるよう
に、その透湿度は厚みに左右される。 このため内層が薄肉に形成された多層容器で
は、容器を形成する樹脂が二軸延伸されたポリエ
チレンテレートであつても、内容物からの吸湿の
影響によつて、中間層によるガスバリヤー性が著
しく減少し、酸素や炭酸ガスの透過度は増大す
る。このためビールや炭酸飲料などの長期保存に
は適さず、また酸素の透過を嫌う食料品や飲物の
容器として使用するには、多層容器であつても更
にガスバリヤー性の向上を図らなければならない
とされている。 (問題点を解決するための手段) この発明は上記多層容器の問題点を解決するた
めに考えられたものであつて、その目的とすると
ころは、従来の多層容器と同様な樹脂を用いる
が、従来構造のものより酸素透過量や炭酸透過量
が一段と少なく、長期間にわたりガスバリヤー性
を維持できることは勿論のこと、比較的高温の状
態下においても、それなりのガスバリヤー性を保
つことができる多層容器の製造方法を提供するこ
とにある。 上記目的によるこの発明の特徴は、ノズル口と
連通した外側流路と、その外側流路の先端部内に
て開口した内側流路とを備えた2重ノズルを用
い、上記内側流路からキヤビテイに有底パリソン
を形成する樹脂を注入し、その樹脂中に、該樹脂
との関連において中間層を形成する他の熱可塑性
樹脂を注入して、中間層が外層側に片寄つて位置
するとともに、その中間層によつて区画形成され
た内層が外層よりも厚肉の少なくとも3層の多層
有底パリソンを成形し、その多層有底パリソンを
延伸吹込成形して、内層が外層よりも著しく厚肉
の多層容器に成形することにある。 (作用) 上記方法では、容器として限られた肉厚のなか
で、外層よりも内層を著しく厚肉に形成すること
ができるから、そこに製造された多層容器は、内
層が外層よりも薄肉に形成されたものよりも、容
器内側から中間層に及ぶ吸湿度の影響は小さく、
また内層を形成する樹脂自体のガスバリヤー性も
向上するなどのことから、多層容器におけるガス
バリヤー性が従来のものより一段と向上する。 更にこの発明を実施例により詳細に説明する。 (実施例) 第1図は全体が3層構造のびん状の多層容器1
を示すもので、内層11及び外層12は同一の熱
可塑性樹脂をもつて形成され、また中間層13は
ガスバリヤー性に優れた熱可塑性樹脂をもつて形
成されている。 上記中間層13は外層12に片寄せて設けら
れ、それにより内層11の肉厚が外層12の肉厚
よりも著しく厚肉となつている。 この内層11と外層12との肉厚は、外層/内
層比1:1.50以上が好ましく、内層が増すほどガ
スバリヤー性が向上する。 上記多層容器1は、パリソン形成樹脂が、その
樹脂の中に注入された他の樹脂による中間層23
によつて、内層21と外層22とに肉厚を異にし
て区画された3層構造の多層有底パリソン2を、
延伸吹込成形することによつて製造することがで
きる。 この多層有底パリソン2は、ノズル口31と連
通した外側流路32と、その外側流路32の先端
部内にて開口した内側流路33とを同心に備えた
2重ノズル3を用いて射出成形される。 従来の2重ノズルを用いた多層有底パリソンの
成形は、外側流路32からパリソン形成樹脂を金
型4に注入しているが、この発明では、従来とは
反対に、内側流路33からパリソン成形樹脂5を
注入し、外側流路32からは中間層形成樹脂6を
注入する。 上記金型4への注入は、第3図に示すように、
まず適量のパリソン成形樹脂5を内側流路33か
ら注入することによつて始められる。 次に第4図に示すように、パリソン成形樹脂5
の注入を一旦停止(0.1〜1.0秒程度)して、中間
層成形用樹脂6を、外側流路32から先に注入し
たパリソン成形樹脂5の中に注入する。 その後、再びパリソン成形樹脂5の注入を開始
して、中間層成形樹脂6と共に注入を行うと、第
5図に示すように、パリソン成形樹脂5が中間層
成形樹脂6によつて内層21と外層22とに区画
され、また中間層23が外層22側に片寄つて位
置する3層構造の多層有底パリソン2が生ずる。 そして、中間層成形樹脂6の注入を停止し、少
量のパリソン成形樹脂5を注入して射出を完了す
ると、底部においても中間層23が内封されたも
のとなる。 上記射出成形工程は、中間層成形樹脂としてエ
チレン・ビニルアルコール共重合体を用いた場合
であるが、メタキシリレン基含有ポリアミドによ
る中間層23を形成する場合には、パリソン成形
樹脂5に続いて中間層成形樹脂6を単独にて注入
し、その後更にパリソン成形樹脂5を注入する。 このような射出成形工程であつても、パリソン
成形樹脂5を内側流路33から注入し、中間層成
形樹脂を外側流路32から注入する限り、内層2
1が外層22よりも著しく厚肉の多層有底パリソ
ン2が生ずる。 次に上記多層有底パリソン2を、通常に延伸吹
込成形して製造した二軸配向の3層容器における
ガスバリヤー効果を示す。 実施例及び比較例 容器の種類 炭酸飲料用丸底びん、0.7、26g、 容器の材料 PET:帝人 TR−8550 PA:MXD−6 ナイロン EVOH:クラレ エバール E−105 酸素・炭酸ガス 透過係数(ボトル当り) c.c./2Kg・24時間・1
気圧 酸素透過測定器 MOCON、2連式ガス透過測定器 炭酸ガス透過測定器 MOCON 5連式ガス透過測定器 (4ボリウム炭酸水充填容器を測定) 測定条件 相対湿度内側 100%RH、 外側65%RH、室温24℃。1週間放置 実施例1、2及び比較例1 容器の組成 外層/中間層/内層 PET/MXD−6ナイロン/PET
(Industrial Application Field) This invention relates to a method for manufacturing a multilayer container made of synthetic resin and having an intermediate layer. (Prior Art) Packaging containers made of synthetic resins made by blow- or stretch-blow molding are lightweight and have drop strength, but they have inferior gas barrier properties compared to glass, and contain contents that do not like the permeation of oxygen, carbon dioxide, etc. When used as a container, further improvements were required. Therefore, a multilayer container having at least three layers has been developed, in which a resin forming the container body is provided with another resin as an intermediate layer to compensate for the defects of the resin. Furthermore, for the intermediate layer, resins such as ethylene/vinyl alcohol copolymers and polyamides, which have excellent gas barrier properties, are used. This multi-layered container can contain an extruded or injection-molded multilayer parison as well as a single-layered container.
It can be made by blow molding or stretch blow molding, with the intermediate layer being located in the middle or inside the resin forming the container body.
In a container body in which this intermediate layer is located in the center, there is no difference in the thickness of the two layers, the inner layer and the outer layer, which are defined by the intermediate layer, but if the intermediate layer is located toward the inside, , there is a difference in the thickness of the inner and outer layers,
The inner layer is significantly thinner than the outer layer. The wall thickness distribution of each layer in a multilayer container is determined by the wall thickness distribution of a multilayer bottomed parison formed by extrusion or injection molding, and the ratio of the wall thickness of the parison directly becomes the ratio of the wall thickness of the container. The molding of multi-layer bottomed parisons was carried out by the Special Publication Publication No. 59-29416.
As described in the publication, a double nozzle having an outer channel communicating with the nozzle opening and an inner channel opening at the tip of the outer channel is used to form a parison. The resin is injected into the cavity from the outer channel, and the intermediate layer forming resin is injected from the inner channel. Also, although the thickness of the intermediate layer can be changed depending on the amount of the two resins injected, the intermediate layer always forms inwardly.
As a result, the inner layer is formed thin. (Problems to be Solved by the Invention) In resins such as ethylene-vinyl alcohol copolymer (EVOH) and polyamide (PA), as the amount of moisture absorbed increases, the amount of permeation of oxygen, carbon dioxide, etc. increases. On the other hand, the biaxially oriented polyester resin used for carbonated beverage bottles has a lower moisture permeability than the above-mentioned resins, but as with all resins, the moisture permeability depends on the thickness. For this reason, in a multilayer container with a thin inner layer, even if the resin forming the container is biaxially stretched polyethylene terate, the gas barrier properties of the intermediate layer may deteriorate due to the influence of moisture absorption from the contents. The permeability of oxygen and carbon dioxide increases. For this reason, they are not suitable for long-term storage of beer and carbonated drinks, and in order to be used as containers for foods and drinks that do not allow oxygen to pass through, even multilayer containers must further improve their gas barrier properties. It is said that (Means for Solving the Problems) This invention was devised to solve the problems of the multilayer containers described above, and its purpose is to use the same resin as the conventional multilayer containers, but The amount of oxygen permeation and the amount of carbon dioxide permeation are much lower than those with conventional structures, and it goes without saying that it can maintain gas barrier properties for a long period of time, and even under relatively high temperature conditions. An object of the present invention is to provide a method for manufacturing a multilayer container. The feature of the present invention for the above-mentioned purpose is to use a double nozzle having an outer flow path communicating with a nozzle opening and an inner flow path opened within the tip of the outer flow path, and to connect the cavity from the inner flow path. A resin forming a bottomed parison is injected, and another thermoplastic resin forming an intermediate layer in relation to the resin is injected into the resin, so that the intermediate layer is biased toward the outer layer, and the intermediate layer is offset toward the outer layer. A multilayer bottomed parison of at least three layers is formed, the inner layer defined by the intermediate layer is thicker than the outer layer, and the multilayer bottomed parison is stretch blow molded to form a parison with an inner layer significantly thicker than the outer layer. The purpose is to form it into a multilayer container. (Function) In the above method, the inner layer can be formed to be significantly thicker than the outer layer within the limited wall thickness of the container. The effect of moisture absorption from the inside of the container to the intermediate layer is smaller than that of the formed one.
In addition, the gas barrier properties of the resin itself forming the inner layer are improved, so that the gas barrier properties of the multilayer container are further improved compared to conventional containers. Further, the present invention will be explained in detail with reference to Examples. (Example) Figure 1 shows a bottle-shaped multilayer container 1 with a three-layer structure as a whole.
The inner layer 11 and the outer layer 12 are made of the same thermoplastic resin, and the intermediate layer 13 is made of a thermoplastic resin with excellent gas barrier properties. The intermediate layer 13 is provided offset to the outer layer 12, so that the inner layer 11 is significantly thicker than the outer layer 12. The thickness of the inner layer 11 and the outer layer 12 is preferably an outer layer/inner layer ratio of 1:1.50 or more, and the gas barrier properties improve as the inner layer increases. The multilayer container 1 has a parison-forming resin and an intermediate layer 23 made of another resin injected into the resin.
A multilayer bottomed parison 2 with a three-layer structure partitioned into an inner layer 21 and an outer layer 22 with different wall thicknesses,
It can be manufactured by stretch blow molding. This multilayer bottomed parison 2 is injected using a double nozzle 3 that is concentrically equipped with an outer flow path 32 communicating with a nozzle opening 31 and an inner flow path 33 opened within the tip of the outer flow path 32. molded. In the conventional molding of a multilayer bottomed parison using a double nozzle, the parison-forming resin is injected into the mold 4 from the outer channel 32, but in this invention, contrary to the conventional method, the parison-forming resin is injected from the inner channel 33. The parison molding resin 5 is injected, and the intermediate layer forming resin 6 is injected from the outer channel 32. The injection into the mold 4 is as shown in FIG.
First, a suitable amount of parison molding resin 5 is injected from the inner channel 33 to begin. Next, as shown in FIG. 4, the parison molding resin 5
The injection is temporarily stopped (about 0.1 to 1.0 seconds), and the intermediate layer molding resin 6 is injected from the outer flow path 32 into the parison molding resin 5 previously injected. Thereafter, when the parison molding resin 5 is again started to be injected together with the intermediate layer molding resin 6, as shown in FIG. A multi-layer bottomed parison 2 having a three-layer structure is produced, in which the intermediate layer 23 is located biased towards the outer layer 22. Then, when the injection of the intermediate layer molding resin 6 is stopped and a small amount of the parison molding resin 5 is injected to complete the injection, the intermediate layer 23 is also encapsulated at the bottom. In the above injection molding process, an ethylene/vinyl alcohol copolymer is used as the intermediate layer molding resin. However, when forming the intermediate layer 23 of metaxylylene group-containing polyamide, the intermediate layer is The molding resin 6 is injected alone, and then the parison molding resin 5 is further injected. Even in such an injection molding process, as long as the parison molding resin 5 is injected from the inner flow path 33 and the intermediate layer molding resin is injected from the outer flow path 32, the inner layer 2
A multilayer bottomed parison 2 is produced in which the outer layer 1 is significantly thicker than the outer layer 22. Next, the gas barrier effect in a biaxially oriented three-layer container manufactured by conventional stretch blow molding of the multilayer bottomed parison 2 will be shown. Examples and Comparative Examples Container type Round bottom bottle for carbonated drinks, 0.7, 26g, Container material PET: Teijin TR-8550 PA: MXD-6 Nylon EVOH: Kuraray Eval E-105 Oxygen/carbon dioxide gas permeability coefficient (per bottle) ) cc/2Kg・24 hours・1
Barometric oxygen permeation meter MOCON, 2-unit gas permeation meter Carbon dioxide permeation meter MOCON 5-unit gas permeation meter (measures a 4-volume carbonated water filled container) Measurement conditions Relative humidity inside 100%RH, outside 65%RH , room temperature 24℃. Examples 1 and 2 and Comparative Example 1 left for one week Container composition Outer layer/middle layer/inner layer PET/MXD-6 nylon/PET

【表】 実施例3、4及び比較例2 容器の組成 外層/中間層/内層 PET EVOH PET【table】 Examples 3, 4 and comparative example 2 Composition of the container Outer layer/middle layer/inner layer PET EVOH PET

【表】【table】

【表】 (発明の効果) この発明では、中間層を外層側に片寄せて位置
させて、内層の肉厚を外層よりも著しく増加さ
せ、その肉厚をもつて内層におけるガスバリヤー
性の向上と、内容物側からの透湿度の低減を図
り、吸湿による中間層のガスバリヤー性の劣化を
防止して、更に一段とガスバリヤー性に優れたも
のとなるから、ビール、炭酸飲料の包装用容器と
して用いた場合、それらの内容物の保存期間を永
くすることができ、酸素透過性の問題から使用さ
れ離かつたケチヤツプやリンゴジユース等の容器
にも用いることができるなど、用途が一段と拡大
する。 また製造に際しても特別な成形技術を要せず、
従来の装置及び成形技術をもつて容易に製造する
ことができるので、特にコスト高となるようなこ
ともないなどの特長を有する。
[Table] (Effects of the Invention) In this invention, the intermediate layer is shifted toward the outer layer, the inner layer is significantly thicker than the outer layer, and this thickness improves the gas barrier properties of the inner layer. This reduces moisture permeability from the contents side, prevents deterioration of the gas barrier properties of the intermediate layer due to moisture absorption, and provides even better gas barrier properties, making it suitable for packaging containers for beer and carbonated drinks. When used as a container, the storage period of the contents can be extended, and the range of uses is further expanded, as it can also be used for containers for ketchup and apple juice, which were previously used due to oxygen permeability issues. . Also, no special molding technology is required for manufacturing.
Since it can be easily manufactured using conventional equipment and molding techniques, it has the advantage of not being particularly expensive.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はこの発明の製造方法による多層容器の
一部拡大部分断面図、第2図は同じく多層有底パ
リソンの部分断面図、第3図から第5図はこの発
明の製造方法における多層有底パリソンの成形工
程を順に示す略示断面図である。 1……多層容器、2……多層有底パリソン、3
……2重ノズル、5……パリソン成形樹脂、6…
…中間層成形樹脂、11……内層、12……外
層、21……内層、22……外層、23……中間
層、31……ノズル口、32……外側流路、33
……内側流路。
FIG. 1 is a partially enlarged partial sectional view of a multilayer container manufactured by the manufacturing method of the present invention, FIG. 2 is a partial sectional view of a multilayer bottomed parison, and FIGS. FIG. 3 is a schematic cross-sectional view sequentially showing the steps of forming the bottom parison. 1...Multilayer container, 2...Multilayer bottomed parison, 3
...Double nozzle, 5...Parison molding resin, 6...
...Intermediate layer molding resin, 11...Inner layer, 12...Outer layer, 21...Inner layer, 22...Outer layer, 23...Intermediate layer, 31...Nozzle opening, 32...Outer channel, 33
...Inner flow path.

Claims (1)

【特許請求の範囲】[Claims] 1 ノズル口と連通した外側流路と、その外側流
路の先端部内にて開口した内側流路とを備えた2
重ノズルを用い、上記内側流路からキヤビテイに
有底パリソンを形成する樹脂を注入し、その樹脂
中に、該樹脂との関連において中間層を形成する
他の熱可塑性樹脂を注入して、中間層が外層側に
片寄つて位置するとともに、その中間層によつて
区画形成された内層が外層よりも厚肉の少なくと
も3層の多層有底パリソンを成形し、その多層有
底パリソンを延伸吹込成形して、内層が外層より
も著しく厚肉の多層容器に成形することを特徴と
する多層容器の製造方法。
1 having an outer flow path communicating with the nozzle opening and an inner flow path opening within the tip of the outer flow path;
Using a heavy nozzle, a resin forming a bottomed parison is injected into the cavity from the inner channel, and another thermoplastic resin forming an intermediate layer in relation to the resin is injected into the resin to form an intermediate layer. Molding a multilayer bottomed parison with at least three layers in which the layers are offset toward the outer layer and the inner layer defined by the intermediate layer is thicker than the outer layer, and stretch blow molding the multilayer bottomed parison. A method for manufacturing a multilayer container, characterized in that the inner layer is significantly thicker than the outer layer.
JP60078015A 1985-04-12 1985-04-12 Multi-layer vessel and manufacture thereof Granted JPS61235126A (en)

Priority Applications (12)

Application Number Priority Date Filing Date Title
JP60078015A JPS61235126A (en) 1985-04-12 1985-04-12 Multi-layer vessel and manufacture thereof
US06/849,556 US4743479A (en) 1985-04-12 1986-04-08 Multi-layered vessels and method for molding the same
CA000506204A CA1271435A (en) 1985-04-12 1986-04-09 Multi-layered vessels and method for molding the same
AU55911/86A AU588581B2 (en) 1985-04-12 1986-04-10 Multi-layered vessels and method for molding the same
KR1019860002713A KR940005636B1 (en) 1985-04-12 1986-04-10 Multi-layer vessel and manufacturing method thereof
DE86400768T DE3688686T2 (en) 1985-04-12 1986-04-10 Forming process Multilayer vessels.
EP86400768A EP0199633B1 (en) 1985-04-12 1986-04-10 Method for molding multi-layered vessels
NZ215789A NZ215789A (en) 1985-04-12 1986-04-11 Triple layered plastics bottle blow moulded from injection moulded parison having thick inner layer
ES553938A ES8704382A1 (en) 1985-04-12 1986-04-11 Method for molding multi-layered vessels.
CN86102410A CN1006773B (en) 1985-04-12 1986-04-12 Multi-layered vessels and method for molding the same
BR8601821A BR8601821A (en) 1985-04-12 1986-04-14 MULTI-LAYER BOTTLES AND METHOD FOR MOLDING THE SAME
US06/941,022 US4774047A (en) 1985-04-12 1986-12-12 Method for molding multi-layered vessels

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60078015A JPS61235126A (en) 1985-04-12 1985-04-12 Multi-layer vessel and manufacture thereof

Publications (2)

Publication Number Publication Date
JPS61235126A JPS61235126A (en) 1986-10-20
JPH053376B2 true JPH053376B2 (en) 1993-01-14

Family

ID=13649965

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60078015A Granted JPS61235126A (en) 1985-04-12 1985-04-12 Multi-layer vessel and manufacture thereof

Country Status (11)

Country Link
US (2) US4743479A (en)
EP (1) EP0199633B1 (en)
JP (1) JPS61235126A (en)
KR (1) KR940005636B1 (en)
CN (1) CN1006773B (en)
AU (1) AU588581B2 (en)
BR (1) BR8601821A (en)
CA (1) CA1271435A (en)
DE (1) DE3688686T2 (en)
ES (1) ES8704382A1 (en)
NZ (1) NZ215789A (en)

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JPS60157826A (en) * 1984-01-27 1985-08-19 Toyo Seikan Kaisha Ltd Manufacture of multilayer drawn bottle

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003054591A (en) * 2001-08-13 2003-02-26 Nippon Synthetic Chem Ind Co Ltd:The Squeezing multi-layered container
JP2003063542A (en) * 2001-08-23 2003-03-05 Nippon Synthetic Chem Ind Co Ltd:The Squeezing-out multi-layer container

Also Published As

Publication number Publication date
JPS61235126A (en) 1986-10-20
CN86102410A (en) 1986-12-03
KR940005636B1 (en) 1994-06-22
CA1271435A (en) 1990-07-10
ES8704382A1 (en) 1987-04-01
ES553938A0 (en) 1987-04-01
EP0199633A3 (en) 1988-10-26
US4743479A (en) 1988-05-10
AU588581B2 (en) 1989-09-21
BR8601821A (en) 1986-12-23
DE3688686D1 (en) 1993-08-19
KR860008017A (en) 1986-11-10
US4774047A (en) 1988-09-27
NZ215789A (en) 1988-04-29
CN1006773B (en) 1990-02-14
EP0199633A2 (en) 1986-10-29
AU5591186A (en) 1986-10-16
DE3688686T2 (en) 1994-02-03
EP0199633B1 (en) 1993-07-14

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